Page 517 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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472                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological



                       10 –2
                                                                     2,4,6-Trichlorophenol
                                                                                  p-Nitrophenol
                                                                           Xylene
                       10 –3                                Benzoic acid  Phenol     n-Butanol
                      Solid phase concentration, X* (mol/g)  10 –4 Hexachlorobutadiene  Bromoform  Dioxane  Urea


                                                    Nitrobenzene


                                                   Carbon tetrachloride
                         –5
                       10
                                                     Chloroform


                       10 –6  Trichloroethylene      Ethylene chloride
                                    Bromochloromethane



                       10 –7
                         10 –9     10 –8    10 –7     10 –6    10 –5    10 –4     10 –3    10 –2     10 –1
                                                  Adsorbate solution concentration C* (mol/L)
            FIGURE 15.10  General isotherm synthesized from specific isotherms. (Adapted from McGuire, M.J. and Suffet, I.H., The calculated net
            adsorption energy concept, Chap. 4, in: Suffet, I. H. and McGuire, M. J. (Eds.), Activated Carbon Adsorption of Organics from the Aqueous
            Phase, Vol. 1, Ann Arbor Science Publishers, Ann Arbor, MI, p. 108, 1980. With permission; see also SDWC (Safe Drinking Water
            Committee), Drinking Water and Health, Vol. 2, National Academy Press, Washington, DC, p. 262, 1980.)






                     C 0
             Bulk of       t 2 >>0
             solution
                                       –
                                       X(r) t >> 0
                                                                       BOX 15.1
                   ( t>>0)                                                       NOMENCLATURE ON C 0
                 C i
                                                                  The term, C 0 , is most often used as a ‘‘starting concen-
                                                                  tration,’’ e.g., with respect to distance or time, for vari-
                            t 1 =0
                                                                  ous kinds of situations. In the case of diffusion to and
                  C (t=0)
                   i
                                                                  within a particle, C 0 is designated here the adsorbate
                                                                  concentration in the ‘‘bulk-of-solution,’’ e.g., as in Fig-
                                    –
                                                                  ure 15.11. In the case of a ‘‘packed bed,’’ the starting
                                    X(r) t =0
                                                                  concentration at the top of the column is also designated
                                             r o
                                                r                 C 0 , in which case the particle usually is not considered
                                                                  and so the distinction in terms is not an issue. For a
                                      Adsorbent                   particle in a packed bed, however, the ‘‘local’’ concen-
                                       particle
                                                                  tration at some depth, Z, is designated C,or C(Z), which
                                                                  is the same as the ‘‘bulk-of-solution’’ concentration, C 0 ,
                                                                  in Figure 15.11. The context in the use of C 0 gives the
                                          Liquid film             distinction. But, if the two models, e.g., packed-bed and
                                                                  particle, are ‘‘linked,’’ as in a computer algorithm, the
                                                                  distinction is necessary. The same ideas hold true for a
            FIGURE 15.11 Concentration gradients across aqueous film and in  ‘‘batch reactor.’’
            solid phase from bulk of solution.
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